Synthetically modified thermoplastic polymer composites having cellulose nanomaterials

ABSTRACT

A method of manufacturing a polymer coated cellulose nanocrystal composite material begins with an aqueous cellulose nanocrystal (CNC) suspension mixture. The aqueous CNC suspension mixture is dried to remove the liquid solvent from the aqueous CNC suspension mixture to form a dry CNC powder. Diethylenetriamine (DETA) is combined with melted Maleated-anhydride Polypropylene (MAPP) to form a DETA-functionalized MAPP (MA) mixture. The MA mixture is cooled and pelletized to form MA pellets. The MA pellets, the dry CNC powder, and a neat polypropylene (PP) are combined to form a CNC-PP mixture. The CNC-PP mixture is compounded by melting, subsequently cooled and pelletized to form CNC-PP pellets.

CROSS REFERENCE TO RELATED APPLICATIONS

This application claims benefit of U.S. Provisional Application No.62/186,417 filed Jun. 30, 2015. The disclosure of the above applicationis incorporated herein by reference.

GOVERNMENT SUPPORT CLAUSE

This invention was made with government support under Contract Number1416493 awarded by the National Science Foundation. The government hascertain rights in the invention.

FIELD

The invention relates to polymer composites and more specifically topolymer composites reinforced with cellulosic nanomaterials.

BACKGROUND

The statements in this section merely provide background informationrelated to the present disclosure and may or may not constitute priorart.

Cellulosic nanomaterials (CN), are the smallest member of the overallhierarchy of cellulose materials and are the most abundant biopolymer.Having high tensile strength and elastic modulus, CN is useful inreplacing higher cost and lower strength material, such as carbon orglass fiber, in polymeric composites. Cellulose nanocrystals (CNC), as asubset of CN, are highly ordered nano-scale crystals remaining aftertreatment to remove disordered amorphous regions from nanofibrils (thenext member of the cellulose hierarchy). However, due to the intrinsichydrophilic nature of CNC the use of CNC in polymer composites hasproven challenging. Poor interfacial adhesion between the CNC and thepolymer and poor dispersion of the CNC in the matrix contributes tolower tensile strength and elastic modulus of the composite than wouldotherwise be possible. Additionally, traditional materials used inpolymer composites require high amounts of energy to produce. Forexample, glass fibers, among the most energy-efficient materials,require 48 MJ/kg to produce compared to 20 MJ/kg required to produceCNC.

Thermoplastics and thermoplastic composites are used widely in myriad ofglobal markets. Polyolefins form an especially robust segment of thisindustry, comprising greater than 50% of the global thermoplasticsmarket. An increased focus on improving sustainability, as well aspersistent economic pressures, drive the need for continuous innovationin this space. In addition to low materials costs, automotive companiesas well as electronic device, building-construction, and consumerproducts manufacturers rely on advantages provided by the selection ofpolyolefin resins for thermoplastic composites. For this reason, thereare myriad advantages present in the thermoplastic processing space,from highly automated equipment which contributes to low cycle-times andlabor requirements to the presence of a mature, global supplier base.These have all contributed to propagate thermoplastic composites intoapplications with increasingly demanding specifications.

While current polymer composites achieve their intended purpose, thereis a need for an improved strength, cost-effective, energy-effective,bio-based polymer composite.

SUMMARY

A method of manufacturing a polymer coated cellulose nanocrystalcomposite material is provided. The method includes providing an aqueouscellulose nanocrystal (CNC) suspension mixture. A next step of themethod includes drying the aqueous CNC suspension mixture to remove theliquid solvent from the aqueous CNC suspension mixture to form a dry CNCpowder. The method next combines an Amine to melted Maleated-anhydridePolypropylene (MAPP) to form a Amine-functionalized MAPP (MA) mixture.The MA mixture is cooled and pelletized to form MA pellets. The MApellets, the dry CNC powder, and a neat polypropylene (PP) are combinedto form a CNC-PP mixture. The CNC-PP mixture is compounded by melting.The CNC-PP mixture is cooled and pelletized to form CNC-PP pellets.

In one aspect of the present invention, drying the aqueous CNCsuspension mixture to remove the liquid solvent from the aqueous CNCsuspension mixture to form a dry CNC powder further includes drying theaqueous CNC suspension mixture by at least one of freeze drying, spraydrying, and solvent drying the aqueous CNC suspension mixture.

In another aspect of the present invention, the step of combining anAmine to melted Maleated-anhydride Polypropylene (MAPP) to form aAmine-functionalized MAPP (MA) mixture further includes combining Amineand MAPP at a weight percent ratio MAH:NH₂ of between 2:1 to 1:3.

In yet another aspect of the present invention, the step of combiningthe MA pellets, the dry CNC powder, and a neat polypropylene (PP) toform a CNC-PP mixture further includes combining the MA pellets and thedry CNC powder at a weight percent ratio CNC:MA of between 1:2 to 1:19.

In yet another aspect of the present invention, the step of compoundingthe CNC-PP mixture by melting further includes compounding the CNC-PPmixture in a high shear environment.

In yet another aspect of the present invention, the step of providing anaqueous cellulose nanocrystal (CNC) suspension mixture further includesproviding a CNC suspension mixture wherein a CNC of the CNC suspensionmixture is highly crystalline, has a rectangular shape, and has adensity of about 1.6 g/cm³.

In yet another aspect of the present invention, the step of providing anaqueous cellulose nanocrystal (CNC) suspension mixture further includesproviding a CNC suspension mixture wherein a CNC of the CNC suspensionmixture is thermally stable in a nitrogen environment up to 250° C., inan atmospheric environment up to 230° C. and has a strong negativesurface charge of −45±1.8 mV.

In yet another aspect of the present invention, the step of combiningthe MA pellets, the dry CNC powder, and a neat polypropylene (PP) toform a CNC-PP mixture further comprises combining the MA pellets and thedry CNC powder at a weight percent ratio CNC:MA of between about 1:5 toabout 1:10.

In yet another aspect of the present invention, a polymer coatedcellulose nanocrystal is provided. The polymer coated cellulosenanocrystal includes a cellulose nanocrystal (CNC) and having a strongnegative charge on a surface of the CNC, and a plurality ofAmine-functionalized MAPP (MA). The CNC is highly crystalline. Theplurality of MA is disposed on the surface of the CNC.

In yet another aspect of the present invention, the CNC has a density ofabout 1.6 g/cm³.

In yet another aspect of the present invention, the CNC is thermallystable in a nitrogen environment up to 250° C., in an atmosphericenvironment up to 230° C., and has a strong negative surface charge of−45±1.8 mV.

In yet another aspect of the present invention, the plurality of MAincludes each of the Amine and Maleated-anhydride Polypropylene (MAPP).

In yet another aspect of the present invention, a weight percent ratioof CNC:MA is from about 1:5 to about 1:10.

Other aspects and advantages of the invention will be explained infurther detail by reference to the following description and appendeddrawings.

DRAWINGS

The drawings described herein are for illustration purposes only and arenot intended to limit the scope of the present disclosure in any way.

FIG. 1 illustrates a plurality of cellulose nanocrystals (CNC) accordingto the principles of the present invention;

FIG. 2 illustrates a polymer-coated cellulose nanocrystal (CNC)according to the principles of the present invention;

FIG. 3 is a graphical representation of DETA-MA-CNC functionalizationaccording to the principles of the present invention;

FIG. 4 is a flowchart depicting a method of producing stabilizedcellulose nanocrystal according to the principles of the presentinvention.

FIG. 5 is a table illustrating a Design of Experiments for DETA-MA-CNCcomposites according to the principles of the present invention;

FIG. 6 includes graphs illustrating test data of MAH:NH₂ and CNC:MAaccording to the principles of the present invention;

FIG. 7 includes graphs illustrating test data of mechanical strength ofMAH:NH₂ and CNC:MA according to the principles of the present invention;

FIG. 8 includes graphs illustrating test data of mechanical strength ofCNC composites according to the principles of the present invention, and

FIG. 9 includes photos of microstructure of CNC composites according tothe principles of the present invention.

DETAILED DESCRIPTION

The following description is merely exemplary in nature and is notintended to limit the present disclosure, application, or uses.

Referring to FIG. 1, a plurality of cellulose nanocrystals (CNC) 2 areillustrated and will now be described. For example, the cellulosenanocrystals (CNC) 2 of FIG. 1 are shown after treatment to separatedisordered amorphous regions (not shown) from the nanofibrils orcellulosic nanomaterials (CN). The dimensions of the CNC 2 areapproximately 3 to 5 nm in width W and 100 to 300 nm long L. The CNC 2are highly crystalline, roughly rectangular, and have a low density ofabout 1.6 g/cm³. Other characteristics of CNC 2 include thermalstability in a nitrogen environment up to 250° C., in air up to 230° C.and a strong negative surface charge of −45±1.8 mV due to residualsulfate esters remaining after the sulfuric acid treatment used toseparate the CNC from the disordered amorphous material.

Turning now to FIG. 2, a polymer coated cellulose nanocrystal isillustrated and generally indicated by reference number 10. The polymercoated cellulose nanocrystal 10 includes a cellulose nanocrystal (CNC) 2and a plurality of DETA-functionalized MAPP (MA) chains 18.Additionally, the plurality of DETA-functionalized MAPP (MA) chains 18are bonded to the cellulose nanocrystal (CNC) 2 and include a Maleicacid (MAH) chain 14, a Maleated-anhydride Polypropylene (MAPP) chain 16,and Diethylenetriamine (DETA) chain 12. More particularly, aPolypropylene (PP) chain is modified by a plurality of MAH chains 14becoming Maleated-anhydride Polypropylene (MAPP) 16. Next, each of aplurality of Diethylenetriamine (DETA) chains 12 are bonded to theMaleated-anhydride Polypropylene (MAPP) chain 16 via each of the Maleicacid chains 14.

Referring now to FIGS. 3 and 4, a method 100 of preparation of polymercoated cellulose nanocrystal is illustrated and will now be described.The method 100 includes a first step 102 of providing an aqueous CNCsuspension. The aqueous solution CNC was obtained from Forest ProductsLaboratory (Madison, Wis.). A second step 104 includes freeze drying,spray drying, and solvent drying the stabilized aqueous cellulosenanocrystal (CNC) suspension mixture until a liquid solvent of thestabilized aqueous cellulose nanocrystal (CNC) suspension is sublimated.A third step 106 includes adding a measured amount of DETA to a measuredamount of melted MAPP (FIGS. 3 (a) and (b)) forming DETA-functionalizedMAPP (MA) (FIG. 1(c)). While the present example of the inventionincludes using DETA, use of other Amines or Amine groups is conceivablewithout departing from the scope of the invention. For example,Triethylenetetramine (TETA) may be used to form an Amine-functionalizedMAPP (MA). A fourth step 108 includes cooling and pelletizing, theDETA-functionalized MAPP (MA) mixture. A fifth step 110 includesfabricating the CNC-PP composites by adding DETA-functionalized MAPP(MA) (FIG. 3(d)) with varying amounts of dried, powderized CNCs (FIG.3(e)) and neat PP and melt compounding (FIG. 3(f)). A sixth step 112includes cooling and pelletizing the mixture. The melt mixing isperformed in a high-shear environment.

Referring now to Table 1 of FIG. 5, Table 1 presents the design ofexperiments for identifying the ideal mix ratios of MAH:NH₂ for thethird step 106 (Column 2 of Table 1) and CNC:MA for the fifth step 110(Column 3 of Table 1). Regarding the third step 106 of the method 100,four principle mix ratios of maleic-acid to amine groups (MAH:NH₂) whichwere tested in order to determine both a process-capable mix (e.g. amixture which would produce a coherent, continuous strand which could beused in subsequent steps) and a trend in which the benefits of thepresence of amine groups to the overall composite could be determined.The mix ratios are 2:1 MAH:NH₂, 1:1 MAH:NH₂, 1:2 MAH:NH₂ and 1:3 MAH:NH₂(MA) and are denoted Reactions 1-4, respectively. The reactionprogressed in the barrel of the melt-compounder at 200° C., in ahigh-shear environment which produced a strand of melted polymer whichwas water-cooled, air-dried and pelletized.

Regarding the fifth step 110, there were four principle mix ratios of MAto CNCs which were mixed with neat PP and fed into the melt-compounder.These mix ratios were selected in order to discern which were morelikely to completely cover the CNCs with the MA, which itself wasdesigned to mix with neat PP to provide a good dispersion. The mixratios are 1:2, 1:5, 1:9, 1:10, and 1:19 CNC:MA. This secondary step wascarried out in the same high-shear environment, producing a strand ofmelted MA-CNC-PP polymer composite which was water-cooled, air-dried andpelletized.

Referring now to Column 1 of Table 1, the Design of Experiments furtherincludes composites loaded at 2, 5 and 10 wt % (CNC wt %). Composites ofall possible recipes were fabricated at 2 wt % CNCs, with fabrication ofthe most promising 5 wt % and 10 wt % recipes following. Finally, themix ratios of the composites at 10 wt % governed that 1:9 was thehighest mixing ratio of CNC:MA possible (e.g. no neat PP in theserecipes); similarly, 5 wt % was the highest mix ratio possible of the1:19 CNC:MA composites (e.g. no neat PP in this recipe). Prior toperforming reaction-extrusion, various MAH:NH₂ recipes were prepared ina batch-reaction method. In measures of 200 g, each recipe was preparedin THF under a fume hood in order to prove reaction progression. Themixtures were heated at 85° C. and stirred vigorously with a spatula forfive hours in early samples and 14 hours for the remaining samples. TheTHF was then decanted off and the precipitate powder was dried andanalyzed by an IR infrared spectrometer which performedFourier-Transform Infrared Spectroscopy (FTIR). Once suitable MAH:NH₂ratios were selected, these recipes were fabricated without solvent inthe melt-compounder. Subsequent to melt-compounding, a composite pelletfrom each recipe was heated and pressed into a thin-film, approximately100 μm thick, and also analyzed by FTIR to confirm a similar extent ofreaction occurred in the high-shear environment.

During the process of melt-mixing, there is a thermodynamicallyfavorable condensation reaction between the amine groups on theTriethylenetetramine (TETA) and the anhydride side groups on the PP.Both primary and secondary amines are present in the TETA and these seekto cleave the oxygen from the cyclic anhydride, forming secondaryamides. The graphs of FIG. 6 illustrate the IR spectra for this reactionwith both the MAH:NH₂ and the CNC:MA reaction discussed. In the firstgraph 200, the formation of peaks in the IR spectra at 1540 cm-1 202 and1580 cm-1 204 are evidence of the MAH:NH₂ reaction progression. The peakfor the reaction ratio of 1:1 MAH:NH₂ was the strongest indicating themost complete reaction. In the second graph 300, the formation of thepeak at 1700 cm-1 302 for the 1:10 CNC:MA and its subsequentstrengthening for the 1:19 CNC:MA indicates increased symmetric carbonylimide stretching as increased MA is mixed with CNCs in the PP. The peaksat 1540 cm-1 304 and 1580 cm-1 306 are maintained for the 1:10 CNC:MAand the 1:19 CNC:MA indicating the presence of amides as well.

Five samples of each recipe were analyzed via tensile testing accordingto ASTM D638. The stress-strain plots 400, 500 of FIG. 7 show themechanical strength of representative specimens containing 5 wt %nanoparticles and 2 wt % nanoparticles. Tensile tests were performed onan Instron Model 3345 load frame with a 5 kN load cell per ASTM D638with a crosshead speed of 5.0 mm/min. At least five specimens of eachsample recipe were analyzed at each loading (2, 5 and 10 wt %). Specimendimensions were taken with a Mitutoyo digital micrometer, with 1 μmaccuracy. The specimens were tested as injected, pulled from ahighly-polished hardened-steel mold. Scanning electron microscopy (SEM)was performed using a JEOL JSM-7500F cold emission microscope onrepresentative fracture surfaces from the 5 wt % tensile-test bars.

The tensile curves were taken from samples mixed at 1:10 CNC:MA ratio,and indicate the increase in tensile strength and elastic modulus asincreasing amines are introduced to the MAPP. Importantly, overallductility in the polymer is maintained at >10% strain-to-failure,substantiating the value of the chemical functionalization (e.g. ifthere were no benefit to the chemistry, the presence of the highlycrystalline nanoparticle would increase modulus to the detriment of bothultimate tensile strength and % elongation). The 1:3 MAH:NH2 presentedthe highest tensile strength and modulus. The graphs 400, 500 of FIG. 7illustrate the improvement in mechanical behavior as the CNCs are morecompletely coated with functionalized MA, relative to non-functionalizedPP. As the particle coverage increases the ultimate tensile strength andelastic modulus are both increased concurrently and this trend issupported by behavior at the other nanoparticle loadings (e.g. with both2 wt % and 5 wt % CNCs the mechanical properties of the compositeincrease both with increasing NH2 and more complete particle coverage).This behavior is likely due to the presence of increased covalentlinkages and electrostatic interactions at the particle-polymerinterface. A related effect derives from increased inter-chain hydrogenbonding as there is a higher quantity of hydrogen-oxygen interactionsdue to increased imide/amide presence.

Referring now to FIG. 8, illustrations of the modulus and tensilestrength values are given and will now be discussed. Values are shownfor neat PP (left-most data in each plot) followed by composites loadedwith 2, 5 and 10 wt % nanocrystals. The error bars represent ±1 standarddeviation. Graphs 600 and 700 of FIG. 8 present the average tensilemodulus and tensile strength of 1:10 CNC:MA composites, fabricated from1:2 MAH:NH₂ polymer. The elastic modulus increased slightly withincreasing amounts of CNCs in the absence of MA 602 but there is littlestatistical difference above 2 wt % 604. Dramatic increases in stiffnessare exhibited when the CNCs are present with MA chemistry 604 as theelastic modulus increases 116% (from 895 to 1933 MPa) 606. The effect ofthe chemistry described in this study is evident from these figures,particularly for the tensile strength values, which increase by 38%(from 25.0 to 34.4 MPa) at 5.5% strain for the 1:10 CNC:MA composites702. The lack of helpful chemistry is evident from the decrease intensile strength as additional nanoparticles are added in the absence ofthe MA chemistry 704. It is common for stiff particles to increase thestiffness of polymeric composites but for improved tensile strength itis necessary to impart improved interfacial adhesion achieved mosteffectively by way of covalent linkages, which implies enhancements inthe chemistry of the composite. Graphs 800 and 900 of FIG. 8 describethe effect on the composite when one component of the recipe is removed,as neat PP is plotted along with various composites at differing MAparticle coverage ratios (1:2, 1:5, and 1:10 CNC:MA addition ratios).The tensile modulus for composites with 1:1 MAH:NH2 CNC:MA loaded with 5wt % CNCs 802, 902 is shown and compared against the tensile modulus ofPP-MAPP co-polymers and with 1:10 CNC-MAPP-PP composites 804, 904 (e.g.composites fabricated with no DETA). The processing parameters were keptconsistent between the runs, for example the MAPP was melt-compoundedwith neat PP in the first step, cooled and pelletized, and the CNCs wereadded in a second compounding step to impart consistent heat-historiesto the composites. The tensile strength is shown analogously in graph900.

Further regarding FIG. 8, considering the PP:MAPP composites, given thediffering molecular weights and degree of branching between neat PP andit was critical to investigate the effect of simply co-extruding the twopolymers together. As expected there was a very modest effect onmechanical properties overall, and the increases seen can be explainedby the higher molecular weight of the MAPP. Regarding the CNC+MAPPcomposites, only 1:10 CNC:MAPP recipes were fabricated due to materialconstraints. The moderate mechanical property improvements from theaddition of the MAPP are most likely due to the interaction with thesecondary bond interaction between OH— groups which are of lowerbond-strength than the covalent linkages formed from the secondaryamides in the DETA-MA-CNC composites.

Turning now to FIG. 9, scanning electron micrographs of the fracturesurfaces of tensile-test specimens are illustrated. FIG. 9(a) shows themicrostructure of unfilled PP, FIG. 9 (b) shows the fracture surfacewith untreated CNCs in PP, FIGS. 9 (c) and (d) shows the evolution ofthe microstructure as levels of NH₂ are increased. In the compositecontaining untreated CNCs, PP-rich/CNC-poor regions are evident asregions of agglomerated CNCs are clearly visible (FIG. 9(b)). The PPsurface appears glassy, while the CNC-rich areas have a granular look.Additionally, multiple crystals can be seen in the fracture surface(FIG. 9(b) inset). It appears that the failure mode was particlepull-out, with the shape and morphology of the individual crystalsmatching that reported elsewhere. FIG. 9(c) depicts a composite with aCNC:MA ratio of 1:5 and FIG. 9(d) depicts a composite with a CNC:MAratio of 1:10. The amine-functionality has a direct effect on themicrostructure of the composite, with individual nanoparticles no longerdistinguishable. The morphology of the failures for the composites withincreased amine content is more ductile in nature, as evidenced byout-of-focus regions in the deeper field of view (e.g. there is agreater portion of the micrograph which is out-of-focus indicative ofincreased ductility in the failure). The composite containing untreatedCNCs has failed at the particle-polymer interface whereas the compositeswhich have been treated with DETA appear to have failed at thepolymer-polymer interface. Evidence for this is observed in thefibrillar morphology shown in the FIGS. 9(c) and (d) insets.

The specific gravity of natural fillers compared to glass and othermineral fillers and dispersion aids is a further advantage of using alow aspect ratio natural filler as a processing/dispersion aid. Forexample, cellulose has a specific gravity of 1.6, whereas glass fiberhas a specific gravity of approximately 2.5.

Many nanoparticles are able to stiffen thermoplastic matrices and gainshave been reported with both renewable and synthetically-derivedparticles. In the present study, DETA has been used to alter thefunctionality of cyclic maleated-anhydride side groups attached topolypropylene. Cellulose nanocrystals were then added andmelt-compounded in a later step. The results of this combined chemistryimproved stiffness by 116% and tensile strength by 38%, whilemaintaining a high strain-at-break value (>10% for composites loaded at5 wt %). The formation of covalent linkages at the particle surface, inconjunction with secondary bond interactions, synergisticallystrengthens and stiffens PP composites. Additive manufacturing,automotive applications, construction materials and consumer productsare likely to benefit from the improved properties afforded by usingthis solvent-free system to disperse/strengthen cellulose nanocrystalsin polypropylene.

The description of the invention is merely exemplary in nature andvariations that do not depart from the spirit of the invention areintended to be within the scope of the invention. Such variations arenot to be regarded as a departure from the spirit and scope of theinvention.

We claim:
 1. A method of manufacturing a polymer coated cellulosenanocrystal composite material, the method comprising: providing anaqueous cellulose nanocrystal (CNC) suspension mixture; drying theaqueous CNC suspension mixture to remove the liquid solvent from theaqueous CNC suspension mixture to form a dry CNC powder; combining anAmine to melted Maleated-anhydride Polypropylene (MAPP) to form anAmine-functionalized MAPP (MA) mixture at a weight percent ratio ofMaleic acid (MAH):NH₂ of between 2:1 to 1:3; cooling and pelletizing theMA mixture to form MA pellets; combining the MA pellets, the dry CNCpowder, and a neat polypropylene (PP) to form a CNC-PP mixture;compounding the CNC-PP mixture by melting, and cooling and pelletizingthe CNC-PP mixture to form CNC-PP pellets.
 2. The method ofmanufacturing a polymer coated cellulose nanocrystal of claim 1, whereindrying the aqueous CNC suspension mixture to remove the liquid solventfrom the aqueous CNC suspension mixture to form a dry CNC powder furthercomprises drying the aqueous CNC suspension mixture to remove the liquidsolvent from the aqueous CNC suspension mixture to form a dry CNC powderby at least one of freeze drying, spray drying, and solvent drying theaqueous CNC suspension mixture.
 3. The method of manufacturing a polymercoated cellulose nanocrystal of claim 1, wherein combining the MApellets, the dry CNC powder, and a neat polypropylene (PP) to form aCNC-PP mixture further comprises combining the MA pellets, the dry CNCpowder, and a neat polypropylene (PP) to form a CNC-PP mixture whereincombining the MA pellets and the dry CNC powder is at a weight percentratio CNC:MA of between 1:2 to 1:19.
 4. The method of manufacturing apolymer coated cellulose nanocrystal of claim 1, wherein compounding theCNC-PP mixture by melting further comprises compounding the CNC-PPmixture by melting in a high shear environment.
 5. The method ofmanufacturing a polymer coated cellulose nanocrystal of claim 1, whereinproviding an aqueous cellulose nanocrystal (CNC) suspension mixturefurther comprises providing an aqueous cellulose nanocrystal (CNC)suspension mixture wherein a CNC of the CNC suspension mixture is highlycrystalline, has a rectangular shape, and has a density of about 1.6g/cm³.
 6. The method of manufacturing a polymer coated cellulosenanocrystal of claim 1, wherein providing an aqueous cellulosenanocrystal (CNC) suspension mixture further comprises providing anaqueous cellulose nanocrystal (CNC) suspension mixture suspensionmixture wherein a CNC of the CNC suspension mixture is thermally stablein a nitrogen environment up to 250° C., in an atmospheric environmentup to 230° C. and has a strong negative surface charge of −45±1.8 mV. 7.The method of manufacturing a polymer coated cellulose nanocrystal ofclaim 1, wherein combining the MA pellets, the dry CNC powder, and aneat polypropylene (PP) to form a CNC-PP mixture further comprisescombining the MA pellets, the dry CNC powder, and a neat polypropylene(PP) to form a CNC-PP mixture wherein the MA pellets and the dry CNCpowder are at a weight percent ratio CNC:MA of between about 1:5 toabout 1:10.
 8. A method of manufacturing a polymer coated cellulosenanocrystal composite material, the method comprising: providing anaqueous cellulose nanocrystal (CNC) suspension mixture; drying theaqueous CNC suspension mixture to remove the liquid solvent from theaqueous CNC suspension mixture to form a dry CNC powder using at leastone of freeze drying, spray drying, and solvent drying, and wherein aCNC of the dry CNC powder is highly crystalline and has a rectangularshape; combining an Amine to melted Maleated-anhydride Polypropylene(MAPP) to form an Amine-functionalized MAPP (MA) mixture at a weightpercent ratio of Maleic acid (MAH):NH₂ of between 2:1 to 1:3; coolingand pelletizing the MA mixture to form MA pellets; combining the MApellets, the dry CNC powder, and a neat polypropylene (PP) to form aCNC-PP mixture; compounding the CNC-PP mixture by melting, and coolingand pelletizing the CNC-PP mixture to form CNC-PP pellets.
 9. The methodof manufacturing a polymer coated cellulose nanocrystal of claim 8,wherein combining the MA pellets, the dry CNC powder, and a neatpolypropylene (PP) to form a CNC-PP mixture further comprises combiningthe MA pellets, the dry CNC powder, and a neat polypropylene (PP) toform a CNC-PP mixture wherein combining the MA pellets and the dry CNCpowder is at a weight percent ratio CNC:MA of between 1:2 to 1:19. 10.The method of manufacturing a polymer coated cellulose nanocrystal ofclaim 9, wherein compounding the CNC-PP mixture by melting furthercomprises compounding the CNC-PP mixture by melting in a high shearenvironment.
 11. The method of manufacturing a polymer coated cellulosenanocrystal of claim 10, wherein providing an aqueous cellulosenanocrystal (CNC) suspension mixture further comprises providing anaqueous cellulose nanocrystal (CNC) suspension mixture wherein a CNC ofthe CNC suspension mixture has a density of about 1.6 g/cm3.
 12. Themethod of manufacturing a polymer coated cellulose nanocrystal of claim11, wherein providing an aqueous cellulose nanocrystal (CNC) suspensionmixture further comprises providing an aqueous cellulose nanocrystal(CNC) suspension mixture wherein the CNC of the CNC suspension mixtureis thermally stable in a nitrogen environment up to 250° C., in anatmospheric environment up to 230° C. and has a strong negative surfacecharge of −45±1.8 mV.
 13. The method of manufacturing a polymer coatedcellulose nanocrystal of claim 12, wherein combining the MA pellets, thedry CNC powder, and a neat polypropylene (PP) to form a CNC-PP mixturefurther comprises combining the MA pellets, the dry CNC powder, and aneat polypropylene (PP) to form a CNC-PP mixture wherein the MA pelletsand the dry CNC powder are at a weight percent ratio CNC:MA of betweenabout 1:5 to about 1:10.